Stephen C. McHaney - Odessa TX Steven L. Oetting - Midland TX Karl L. Herzog - Odessa TX
Assignee:
Huntsman Polymers Corporation - Salt Lake City UT
International Classification:
B29B 730
US Classification:
425171
Abstract:
A method and apparatus for product recovery of polyolefins, particularly high molecular weight amorphous poly alphaolefins, wherein the use of water during the method is significantly decreased and wherein the intermediate stage of storing and drying the chunk form of the polyolefin is eliminated. Polyolefins produced in a reactor are heated and mixed by sigma blades in a kneader-extruder to remove any unreacted monomer(s). The polyolefin material in a liquid form is then transferred directly to an extruder to further remove any unreacted monomer(s) and catalyst(s). The invention further includes a method of measuring the inventory in a vessel using a gas of known quantity and known thermodynamic properties.
Process For The Recovery Of Amorphous Devaporized Polyalphaolefin
A circulation loop is provided between a point next to the outlet of an amorphous polyalphaolefin polymerization zone and a flash zone, carrying a stream of molten devaporized polymer product.
Samuel J. Paton - Odessa TX Stephen C. McHaney - Odessa TX Steven L. Oetting - Midland TX Karl L. Herzog - Odessa TX
Assignee:
Huntsman Polymers Corporation - Odessa TX
International Classification:
C08F 600
US Classification:
526 61
Abstract:
Disclosed herein are novel polymers and copolymers of alphaolefins produced using various Ziegler/Natta and Metallocene catalysts. Commercial production of these polymers is now possible for the first time owing to the polymer harvesting technology also disclosed herein.
Amorphous Poly Alpha Olefins Of Low Acid And Organoleptic Properties And A Process For Producing Same
Nick Fowler - Odessa TX, US Enrico Buenacosa - Odessa TX, US John Joseph DeCair - Odessa TX, US Steven Oetting - Odessa TX, US Andres Sustic - Odessa TX, US
International Classification:
C09J 123/14
Abstract:
A process for reducing unreacted monomers and condensable and non-condensable hydrocarbon fractions in an APAO which includes introducing molten APAO into heated and insulated jacketed pipe while injecting a stripping agent based on the total weight of the contents of the jacketed pipe; maintaining the stripping agent with the molten APAO stream from ten seconds to ten minutes, forming a flowable heated mixture at 250 to 450 degrees Fahrenheit in the heated and jacketed pipe forming a flowing heated mixture; and passing the flowing heated mixture through a thin film evaporator assembly, while maintaining the temperature of the flowing heated mixture, stripping the organoleptic species and acids and volatile organic components from the flowing heated mixture and removing and recovering a condensable fuel fraction and a non-condensable hydrocarbon gas with energy, while simultaneously forming an odor-reduced, cleaned molten APAO-based HMA.
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